CN107445321A - Double-micro treatment process for treating oilfield produced water - Google Patents
Double-micro treatment process for treating oilfield produced water Download PDFInfo
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/04—Flow arrangements
- C02F2301/046—Recirculation with an external loop
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/16—Enhanced recovery methods for obtaining hydrocarbons
- E21B43/20—Displacing by water
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Abstract
本发明涉及一种用于处理油田采出水的双微处理工艺。主要解决了现有已经能够达到油田低渗透率油层回注水水质控制指标要求的处理工艺存在的处理工艺较为复杂、处理水质不能够稳定达标的问题。其特征在于:包括以下步骤:(1)含油采出水进入微旋流气浮选器进行油水分离;(2)经过微旋流气浮选器处理后的出水再进入缓冲罐1及微过滤装置,微过滤装置的出水达到油田回注水水质控制指标要求后进入外输水罐;(3)外输水罐中的水经提升对一个过滤周期后微过滤装置中的滤料进行反冲洗再生;(4)微过滤装置排出的反冲洗污水依次进入缓冲罐2、微旋流气浮选器进行再处理。该工艺能够达到油田低渗透率或特低渗透率油层回注水水质控制指标要求。
The invention relates to a double micro-treatment process for treating oilfield produced water. It mainly solves the problem that the existing treatment process that has been able to meet the water quality control index requirements of oilfield low-permeability reservoir reinjection water is relatively complicated and the treatment water quality cannot meet the standard stably. It is characterized in that it includes the following steps: (1) the oil-containing produced water enters the micro-swirl air flotation device for oil-water separation; (2) the effluent treated by the micro-swirl air flotation device enters the buffer tank 1 and the micro-filtration device, and the micro-swirl air flotation device The effluent from the filter device enters the external water transfer tank after meeting the water quality control index requirements of oilfield reinjection water; (3) The water in the external water transfer tank is lifted to backwash and regenerate the filter material in the micro-filtration device after one filtration cycle; (4 ) The backwash sewage discharged from the micro-filtration device enters the buffer tank 2 and the micro-swirl air flotation device for further treatment. The process can meet the water quality control index requirements of reinjection water in low-permeability or ultra-low-permeability reservoirs in oilfields.
Description
技术领域technical field
本发明涉及油田采出水处理技术领域,尤其涉及一种用于处理油田采出水的双微处理工艺。The invention relates to the technical field of oilfield produced water treatment, in particular to a double micro-treatment process for treating oilfield produced water.
背景技术Background technique
目前已有的油田采出水处理技术,采用重力式沉降罐或气浮选进行除油和去除部分悬浮固体,其出水满足后续过滤要求的进水水质;然后再经颗粒粒状滤料过滤器过滤达到油田要求的不同渗透率油层回注水水质控制指标。目前已建极为典型的处理后的最终出水能够达到油田低渗透率或特低渗透率油层回注水水质控制指标要求的处理工艺技术为:重力式沉降罐→气浮选→微生物→一级双层滤料过滤→二级双层滤料过滤→陶瓷膜精细过滤→净化水。At present, the existing oilfield produced water treatment technology adopts gravity settling tank or air flotation to remove oil and remove part of suspended solids, and the effluent meets the influent water quality required by subsequent filtration; then it is filtered through granular filter material filter to reach Reinjection water quality control indicators for different permeability reservoirs required by oilfields. At present, the most typical treatment technology that the final effluent after treatment can meet the water quality control index requirements of low permeability or ultra-low permeability oil layer reinjection water is: gravity settling tank→air flotation→microorganism→first-stage double-layer Filter material filtration→secondary double-layer filter material filtration→ceramic membrane fine filtration→water purification.
此工艺技术从整体来看处理工艺较为复杂,需要经过6段的处理设备才能够将含油污水处理达标,即达到油田低渗透率或特低渗透率油层回注水水质控制指标要求。由此带来的占地面积大、运行费用高,微生物处理后产生的副产物剩余活性污泥很难处理达到环保的要求,而且陶瓷膜经过长时间的运行后其通量衰减较快,以及膜的再生还需要定期进行化学再生从而增加处理设备和复杂的工艺,以及再生过程产生的酸碱废液在系统内循环处理将影响整个系统处理的水质达标。Overall, the treatment process of this process technology is relatively complicated, and it needs to go through 6 stages of treatment equipment to treat the oily sewage up to the standard, that is, to meet the water quality control index requirements of oilfield low permeability or ultra-low permeability oil layer reinjection water. The resulting large area, high operating costs, the residual activated sludge produced by the microbial treatment is difficult to meet the requirements of environmental protection, and the flux of the ceramic membrane decays quickly after a long period of operation, and Membrane regeneration also requires regular chemical regeneration to increase treatment equipment and complex processes, and the acid-base waste liquid generated during the regeneration process will be recycled in the system, which will affect the water quality of the entire system.
另外,上述处理工艺中采用的立式沉降罐的处理效率相对高效的处理设备低、设备体积大和占地面积大;还有就是油田开发后期水中含有化学驱油剂,使得经油水分离后的含油采出水乳化程度高、油珠颗粒细小和油珠浮升速度慢等,采用单一的物理方法实现采出含油污水的油水沉降分离很难达到预期的效果和目的,并由此产生了处理设备的不适应,从而导致处理工艺复杂和工程投资增加;在过滤方面主要使用单层石英砂过滤器和双层滤料过滤器,在水驱处理方面目前还有应用核桃壳及纤维球滤料等过滤器,但也出现对含有化学驱油剂的采出水性质发生变化的不适应,滤料容易板结,再生困难和滤速低等问题的产生。In addition, the treatment efficiency of the vertical settling tank used in the above-mentioned treatment process is relatively low compared with the high-efficiency treatment equipment, and the equipment volume is large and the floor area is large; there is also a chemical oil displacement agent in the water in the late stage of oilfield development, which makes the oily oil after oil-water separation Due to the high degree of emulsification of the produced water, the small size of the oil beads and the slow rise of the oil beads, it is difficult to achieve the expected effect and purpose by using a single physical method to achieve the oil-water sedimentation and separation of the produced oily sewage, which leads to the failure of the treatment equipment. Not suitable, resulting in complicated treatment process and increased engineering investment; in terms of filtration, single-layer quartz sand filters and double-layer filter media filters are mainly used, and walnut shells and fiber ball filter media are currently used in water flooding treatment. However, there are also problems such as inadaptability to changes in the properties of produced water containing chemical oil displacement agents, easy compaction of filter media, difficult regeneration and low filtration rate.
发明内容Contents of the invention
本发明在于克服背景技术中存在的现有已经能够达到油田低渗透率油层回注水水质控制指标要求的处理工艺存在的处理工艺较为复杂、处理水质不能够稳定达标的问题,而提供一种用于处理油田采出水的双微处理工艺。该工艺处理后的油田采出水能够达到油田低渗透率或特低渗透率油层回注水水质控制指标要求,且在达到同等处理效果的前提下,处理设备及工艺技术先进,占地面积小,运行费用低。The present invention aims to overcome the existing problems in the background technology that can meet the water quality control index requirements of low-permeability reservoir reinjection water in the oil field, the processing technology is relatively complicated, and the water quality cannot be stably up to the standard, and provides a method for A dual micro-treatment process for treating oilfield produced water. The oilfield produced water treated by this process can meet the water quality control index requirements of oilfield low permeability or ultra-low permeability oil layer reinjection water, and under the premise of achieving the same treatment effect, the treatment equipment and process technology are advanced, the floor area is small, and the operation low cost.
本发明解决其问题可通过如下技术方案来达到:一种用于处理油田采出水的双微处理工艺,包括以下步骤:The present invention solves its problem and can reach through following technical scheme: a kind of double micro-processing technique for processing oilfield produced water comprises the following steps:
(1)被处理的含油采出水依靠重力或增压泵提升进入微旋流气浮选器进行油水分离去除分散油和部分乳化油及少量的颗粒杂质;(1) The oil-containing produced water to be treated is lifted by gravity or a booster pump into the micro-swirl air flotation device for oil-water separation to remove dispersed oil, partially emulsified oil and a small amount of particulate impurities;
(2)经过微旋流气浮选器处理后的出水再进入缓冲罐1,缓冲罐1的水经提升泵1进入微过滤装置,被处理的采出水在微过滤装置中先后完成调质和反应及过滤的过程;微过滤装置的出水达到油田低渗透率或特低渗透率油层回注水水质控制指标要求后进入外输水罐,再经提升泵3进入注水站进行回注;(2) The effluent treated by the micro-swirl air flotation device enters the buffer tank 1, and the water in the buffer tank 1 enters the micro-filtration device through the lift pump 1, and the treated produced water completes conditioning and reaction in the micro-filtration device. And the process of filtration; the effluent of the microfiltration device reaches the water quality control index requirements of low permeability or ultra-low permeability oil layer reinjection water in the oil field, enters the external water transfer tank, and then enters the water injection station through the lift pump 3 for reinjection;
(3)步骤(2)外输水罐中的水经提升泵4提升对在完成一个过滤周期后的微滤罐中装填的滤料进行反冲洗再生,使滤料恢复原有的截留和吸附能力,然后再进行下一个过滤周期的过滤;(3) Step (2) The water in the external water transfer tank is lifted by the lifting pump 4 to backwash and regenerate the filter material filled in the microfiltration tank after completing a filtration cycle, so that the filter material can restore the original interception and adsorption capacity, and then proceed to the next filtering cycle;
(4)步骤(3)微滤罐装填的滤料反冲洗再生排出的反冲洗污水进入缓冲罐2,再经提升泵5提升进入微旋流气浮选器的进水管线上,进入微旋流气浮选器进行再处理;(4) Step (3) The backwash sewage discharged from the backwash regeneration of the filter material filled in the microfiltration tank enters the buffer tank 2, and then is lifted by the lifting pump 5 to enter the water inlet pipeline of the microcyclone air flotation device, and enters the microcyclone Flow air flotation device for reprocessing;
(5)步骤(1)微旋流气浮选器进行油水分离产生的浮油渣进入浮油渣罐,然后经泵提升进入脱水站进行脱水再处理;微旋流气浮选器底部沉降分离出来的污泥排入污渣罐后进行浓缩,然后外运污泥处理站做进一步的处理达到无害化和资源化利用;(5) Step (1) The scum produced by the oil-water separation of the micro-swirl air flotation device enters the scum tank, and then is lifted by the pump into the dehydration station for dehydration and reprocessing; After the sludge is discharged into the sludge tank, it is concentrated, and then the sludge treatment station for further treatment is carried out to achieve harmless and resourceful utilization;
本发明确定的“微旋流气浮→微过滤装置→净化水”处理工艺,首先是含油采出水进入微旋流气浮装置,微旋流气浮装置是集微旋流技术和气浮选技术于一体的高效处理装置;该装置运行时首先是被处理的含油采出水依靠重力或增压泵提升,经过管道静态混合器(主要是考虑加药时药剂与污水的混合作用),然后再经微旋流气浮选器的进水管线同时与微气泡发生装置产生的微气泡水混合,沿切线方向进入微旋流气浮选器内,并在旋流离心力+气浮浮力的复合作用下进行油珠和杂质的聚集、黏附(微气泡水在压力降低的条件下释放出微气泡与油滴及悬浮固体黏附),从而快速高效地实现离心浮选分离除油及去除悬浮固体杂质。The treatment process of "micro-swirl air flotation → micro-filtration device → purified water" determined by the present invention, firstly, the oily produced water enters the micro-swirl air flotation device, and the micro-swirl air flotation device integrates micro-swirl technology and air flotation technology High-efficiency treatment device; when the device is in operation, the oily produced water to be treated is firstly lifted by gravity or a booster pump, passes through the pipeline static mixer (mainly considering the mixing effect of the chemical agent and sewage during dosing), and then passes through the micro-swirl air The water inlet line of the flotation device is mixed with the micro-bubble water generated by the micro-bubble generating device at the same time, and enters the micro-swirl air flotation device along the tangential direction, and the oil droplets and impurities are removed under the compound action of the swirl centrifugal force + air flotation buoyancy. Aggregation and adhesion (microbubble water releases microbubbles to adhere to oil droplets and suspended solids under the condition of reduced pressure), so as to quickly and efficiently realize centrifugal flotation separation to remove oil and remove suspended solid impurities.
所述微过滤装置是由缓冲调质、反应装置和微滤罐组成,其中的微滤介质采用活性微孔陶瓷镀膜滤料进行过滤处理。而活性微孔陶瓷镀膜滤料具有较大的比表面积和高效吸附污水中的杂质的能力,再加上采用较深的滤床形式,从而使微滤具有较高的纳污能力和较高的过滤精度;另外由于采用脉冲气、水联合反洗对活性微孔陶瓷镀膜滤料进行再生而具有再生效果好和节约大量反冲洗水的特点。The microfiltration device is composed of a buffer conditioning device, a reaction device and a microfiltration tank, wherein the microfiltration medium adopts active microporous ceramic coating filter material for filtration treatment. The active microporous ceramic coating filter material has a large specific surface area and the ability to efficiently absorb impurities in sewage, coupled with the use of a deeper filter bed form, so that the microfiltration has a higher dirt-holding capacity and a higher Filtration accuracy; in addition, due to the use of pulse gas and water combined backwashing to regenerate the active microporous ceramic coating filter material, it has the characteristics of good regeneration effect and saving a lot of backwashing water.
本发明与上述背景技术相比较可具有如下有益效果:采用本发明用于处理油田采出水的双微处理工艺,一方面大大的简化了已有的处理工艺流程,提高了整体处理工艺的处理效果和效率;另一方面,因采用微旋流气浮选器进行油水分离替代了两级沉降除油设备,缩短被处理污水的有效停留时间,同时还可去除污水中的分散油和部分乳化油,而大大节省了设备的占地面积在50%以上,并减少了运行费用;后续去除残余油和残余固体颗粒杂质的过滤方式因为采用微过滤装置,最终能够将含油量平均为147.7mg/L、悬浮固体含量平均35.07mg/L的被处理的采出水,处理后出水含油量为痕迹,悬浮固体含量平均≤1.0mg/L,粒径中值平均0.946μm,达到油田特低渗透率油层“5.1.1” (即:含油量≤5mg/L ,悬浮固体含量≤1mg/L,颗粒粒径中值≤1μm)回注水水质控制指标要求,本发明使用微过滤技术,相比现有采用砂滤过滤技术提高了1~2个数量级的过滤精度(一般砂滤过滤精度大约2-5μm,而微滤的过滤精度可以达到1μm微米以下);另外还解决了使用超滤膜组件存在的膜使用寿命短,水通量衰减快,膜再生困难等生产实际的难题。因此,微旋流气浮及微过滤技术的使用,能够满足外围油田特低渗透率油层的有效开发,确保处理后的含油污水全部回注地下,进一步驱油提高原油采收率,实现了污水的资源化利用和油田的绿色开发。 Compared with the above-mentioned background technology, the present invention can have the following beneficial effects: adopting the double micro-treatment process for treating oilfield produced water of the present invention greatly simplifies the existing treatment process flow on the one hand and improves the treatment effect of the overall treatment process and efficiency; on the other hand, because the micro-swirl air flotation device is used for oil-water separation to replace the two-stage sedimentation oil removal equipment, the effective residence time of the treated sewage is shortened, and the dispersed oil and part of the emulsified oil in the sewage can also be removed. It greatly saves more than 50% of the equipment's floor area and reduces operating costs; the subsequent filtration method for removing residual oil and residual solid particle impurities can finally reduce the oil content to an average of 147.7mg/L, The treated produced water with an average suspended solid content of 35.07mg/L, the oil content of the effluent water after treatment is traces, the average suspended solid content is ≤1.0mg/L, and the average median particle size is 0.946μm, reaching the oilfield ultra-low permeability oil layer "5.1 .1” (ie: oil content ≤ 5mg/L, suspended solids content ≤ 1mg/L, particle size median ≤ 1μm) water quality control index requirements for reinjection water, the present invention uses microfiltration technology, compared with existing sand filtration Filtration technology improves the filtration accuracy by 1 to 2 orders of magnitude (the filtration accuracy of general sand filtration is about 2-5 μm, while the filtration accuracy of microfiltration can reach below 1 μm); in addition, it also solves the problem of using ultrafiltration membrane modules. Short, fast decay of water flux, difficult membrane regeneration and other practical problems in production. Therefore, the use of micro-swirl air flotation and micro-filtration technology can meet the effective development of extra-low permeability oil layers in peripheral oilfields, ensure that all the treated oily sewage is re-injected underground, further oil displacement improves oil recovery, and realizes the recovery of sewage. Resource utilization and green development of oil fields.
说明书附图:Attached to the manual:
附图1 本发明的用于处理油田采出水的双微处理工艺流程示意图。Accompanying drawing 1 is a schematic flow chart of the double micro-treatment process for treating oilfield produced water according to the present invention.
具体实施方式:detailed description:
下面将结合附图及具体实施例对本发明作进一步说明:The present invention will be further described below in conjunction with accompanying drawing and specific embodiment:
如图1所示,该用于处理油田采出水的双微处理工艺,包括以下步骤:As shown in Figure 1, the double micro-treatment process for treating oilfield produced water includes the following steps:
(1)被处理的含油采出水依靠重力(或增压泵提升)进入微旋流气浮选器进行油水分离去除分散油和部分乳化油及少量的颗粒杂质,在进入微旋流气浮选器的进水管线上同时可投加浮选药剂及掺入带有微气泡的回流水,随被处理的污水一同进入微旋流气浮选器;(1) The treated oily produced water enters the micro-swirl air flotation unit by gravity (or booster pump lift) for oil-water separation to remove dispersed oil, partially emulsified oil and a small amount of particulate impurities. After entering the micro-swirl air flotation unit At the same time, flotation reagents and return water with micro-bubbles can be added to the water inlet pipeline, and then enter the micro-swirl air flotation unit together with the treated sewage;
(2)经过微旋流气浮选器处理后的出水再进入缓冲罐1,缓冲罐1的水经提升泵1进入微过滤装置;所述微滤装置是由缓冲调质、反应装置和微滤罐组成;所述微滤罐中填装的微滤介质采用活性微孔陶瓷镀膜滤料进行过滤处理;而活性微孔陶瓷镀膜滤料K80≤1.2,比表面积达到13.6m2/g;微滤罐内部滤床厚度达到3m,微滤的过滤精度为1μm微米以下;在微过滤装置先后完成调质、反应及过滤的过程,在进人微过滤装置的进水管线里投加调质絮凝剂聚合氯化铝,使采出水中的杂质颗粒絮凝形成较大的絮状矾花,从而被后续具有深床过滤特点的活性陶瓷滤料吸附、截留去除,微过滤装置的出水达到油田回注水水质控制指标要求后进入外输水罐,再经提升泵3进入注水站进行回注;(2) The effluent treated by the micro-swirl air flotation device enters the buffer tank 1, and the water in the buffer tank 1 enters the micro-filtration device through the lift pump 1; the micro-filtration device is composed of buffer conditioning, reaction device and micro-filtration Tank composition; the microfiltration medium filled in the microfiltration tank is filtered by active microporous ceramic coating filter material; while the active microporous ceramic coating filter material K80≤1.2, the specific surface area reaches 13.6m 2 /g; microfiltration The thickness of the filter bed inside the tank reaches 3m, and the filtration accuracy of the microfiltration is below 1μm; the process of conditioning, reaction and filtration is completed in the microfiltration device, and the conditioning flocculant is added to the water inlet pipeline of the microfiltration device Polyaluminum chloride flocculates the impurity particles in the produced water to form larger flocculent alum flowers, which are absorbed and retained by the subsequent active ceramic filter material with deep bed filtration characteristics, and the effluent of the microfiltration device reaches the quality of oilfield reinjection water After the control index is required, it enters the external water transfer tank, and then enters the water injection station through the lift pump 3 for reinjection;
(3)外输水罐中的水经提升泵4提升对一个过滤周期后微过滤装置中的微滤罐中装填的滤料进行反冲洗再生,使滤料恢复原有的截留和吸附能力进行下一个过滤周期的过滤;在进行滤料的反冲洗再生过程中,需要将空压机产生的气体掺入到反冲洗中形成气水反冲洗水,从而提高微滤罐中滤料的再生效果;(3) The water in the external water transfer tank is lifted by the lift pump 4 to backwash and regenerate the filter material filled in the microfiltration tank in the microfiltration device after one filtration cycle, so that the filter material can restore its original interception and adsorption capacity. Filtration in the next filtration cycle; in the process of backwash regeneration of the filter material, it is necessary to mix the gas generated by the air compressor into the backwash to form gas-water backwash water, thereby improving the regeneration effect of the filter material in the microfiltration tank ;
(4)微过滤装置中微滤罐反冲洗再生排出的反冲洗污水进入缓冲罐2,再经提升泵5提升进入微旋流气浮选器的进水管线上,进入微旋流气浮选器进行再处理;(4) The backwash sewage discharged from the backwash regeneration of the microfiltration tank in the microfiltration device enters the buffer tank 2, and then is lifted by the lifting pump 5 into the inlet pipeline of the microcyclone air flotation device, and then enters the microcyclone air flotation device for further processing. Reprocessing;
(5)微旋流气浮选器进行油水分离产生的浮油渣进入浮油渣罐,然后经泵提升进入脱水站进行脱水再处理;微旋流气浮选器底部沉降分离出来的污泥排入污渣罐后进行浓缩,然后外运污泥处理站做进一步的无害化处理和资源化利用。(5) The scum produced by the oil-water separation of the micro-swirl air flotation device enters the scum tank, and then is lifted by the pump into the dehydration station for dehydration and reprocessing; the sludge separated from the bottom of the micro-swirl air flotation device is discharged into the The sludge is concentrated after the sludge tank, and then transported to the sludge treatment station for further harmless treatment and resource utilization.
微过滤装置是由缓冲调质、反应装置和微滤罐组成,其中的微滤介质采用活性微孔陶瓷镀膜滤料进行过滤处理。而活性微孔陶瓷镀膜滤料具有较大的比表面积(活性微孔陶瓷镀膜滤料是采用人工烧制的均匀滤料,K80≤1.2,比表面积达到13.6m2/g,是石英砂的100倍以上,大大提高了其表面吸附能力)和高效吸附污水中的杂质的能力,再加上滤罐内部采用较深的滤床形式(滤床厚度达到3m,是核桃壳及石英砂滤床厚度的3倍,实际有效滤程是石英砂的5倍以上,提高了过滤效果),从而使微过滤具有较高的纳污能力和较高的过滤精度(一般砂滤过滤精度大约2-5μm,微滤的过滤精度可以达到1μm以下);另外由于采用脉冲气、水联合反洗对活性微孔陶瓷镀膜滤料进行再生而具有再生效果好和节约大量反冲洗水的特点。后续去除残余油和残余固体颗粒杂质的过滤方式因为采用微过滤装置,最终能够将含油量平均为147.7mg/L、悬浮固体含量平均35.07mg/L的被处理的采出水,处理后出水含油量为痕迹,悬浮固体含量平均≤1.0mg/L,粒径中值平均0.946μm,达到油田特低渗透率油层“5.1.1” (即:含油量≤5mg/L ,悬浮固体含量≤1mg/L,颗粒粒径中值≤1μm)回注水水质控制指标要求。The microfiltration device is composed of buffer conditioning, reaction device and microfiltration tank, and the microfiltration medium adopts active microporous ceramic coating filter material for filtration treatment. The active microporous ceramic coating filter material has a larger specific surface area (the active microporous ceramic coating filter material is a uniform filter material that is artificially fired, K80≤1.2, and the specific surface area reaches 13.6m 2 /g, which is 100 times that of quartz sand. times, greatly improving its surface adsorption capacity) and the ability to efficiently adsorb impurities in sewage, plus the deep filter bed form inside the filter tank (the thickness of the filter bed reaches 3m, which is the thickness of the walnut shell and quartz sand filter bed 3 times that of quartz sand, and the actual effective filtration range is more than 5 times that of quartz sand, which improves the filtration effect), so that microfiltration has high dirt holding capacity and high filtration accuracy (generally, the filtration accuracy of sand filter is about 2-5μm, The filtration accuracy of microfiltration can reach below 1μm); in addition, because the pulse gas and water combined backwashing are used to regenerate the active microporous ceramic coating filter material, it has the characteristics of good regeneration effect and saving a lot of backwashing water. Subsequent filtration method for removing residual oil and residual solid particle impurities can finally reduce the treated produced water with an average oil content of 147.7mg/L and an average suspended solid content of 35.07mg/L, and the oil content of the treated effluent For traces, the average suspended solid content is ≤1.0mg/L, and the average particle size is 0.946μm. , median particle size ≤ 1μm) Reinjection water quality control index requirements.
经微过滤装置处理后的水质最终能够达到油田水驱低渗透率或特低渗透率油层回注水水质控制指标要求,再经注水井回注地下补充地层亏空和达到驱油提高采收率的目的,避免污水外排所造成的环境污染和经济罚款,实现含油污水的有效处理及污水的资源化利用,确保处理后的污水全部回注地下,进一步提高原油采收率,实现油田的绿色开发。The water quality treated by the micro-filtration device can finally meet the water quality control index requirements of oilfield water flooding low permeability or ultra-low permeability oil layer reinjection water, and then reinjection underground through water injection wells to supplement the formation deficit and achieve the purpose of oil displacement and enhanced recovery , avoid environmental pollution and economic fines caused by sewage discharge, realize effective treatment of oily sewage and resource utilization of sewage, ensure that all treated sewage is reinjected into the ground, further increase crude oil recovery, and realize green development of oil fields.
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Application publication date: 20171208 |